Adsorption of CO2 from dry gases on MCM-41 silica at ambient temperature and high pressure. 2: Adsorption of CO2/N2, CO2/CH4 and CO2/H2 binary mixtures

被引:133
|
作者
Belmabkhout, Youssef [1 ]
Sayari, Abdelhamid [1 ]
机构
[1] Univ Ottawa, Dept Chem, Ottawa, ON K1N 6N5, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Adsorption; Porous media; Separation; Selectivity; IAST; PSA; METAL-ORGANIC FRAMEWORKS; CARBON-DIOXIDE; MOLECULAR SIMULATION; COMPUTER-SIMULATION; PORE-SIZE; FLUE-GAS; SEPARATION; METHANE; CH4; EQUILIBRIUM;
D O I
10.1016/j.ces.2009.05.039
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Adsorption equilibrium capacity of CO2, CH4, N-2, H-2 and O-2 on periodic mesoporous MCM-41 silica was measured gravimetrically at room temperature and pressure up to 25 bar. The ideal adsorption solution theory (IAST) was validated and used for the prediction of CO2/N-2, CO2/CH4, CO2/H-2 binary mixture adsorption equilibria on MCM-41 using single components adsorption data. In all cases, MCM-41 showed preferential CO2 adsorption in comparison to the other gases, in agreement with CO2/N-2, CO2/CH4, CO2/H-2 selectivity determined using IAST. In comparison to well known benchmark CO2 adsorbents like activated carbons, zeolites and metal-organic frameworks (MOFs), MCM-41 showed good CO2 separation performances from CO2/N-2, CO2/CH4 and CO2/H-2 binary mixtures at high pressure, via pressure swing adsorption by utilizing a medium pressure desorption process (PSA-H/M). The working CO2 capacity of MCM-41 in the aforementioned binary mixtures using PSA-H/M is generally higher than 13X zeolite and comparable to different activated carbons. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:3729 / 3735
页数:7
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